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Avert Steam Pipeline And Piping Failure And Steam Leaks In The Field

机译:避免蒸汽管道和管道故障和蒸汽泄漏在现场

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Steam piping and pipeline whipping, bowing, buckling and jumping are some of the phenomenon observed in the field due to improper design and inadequate commissioning procedures. As a result, ‘steam flood’, ‘cyclic steam stimulation’ and ‘SAGD’ operations experiences long steaming hold‐ups, extended shutdowns, production losses and environmental clean‐up Steam pipelines up to 32” diameter and 30 km length, with 11 ‐ 15 MPa design pressure and 250‐340 deg C design temperature for quality of steam from 80 to 100%, are being designed with high strength material and thin wall designs. Although, designs are robust and utilizes proven stress analysis tools, but are often fail to address the common field issues of unequal warming, condensate buildup and severe slugging encountered during the commissioning and at the start of the new steaming cycle. Also, piping connections lack the provision to accommodate requisite thermal growth and/or the unequal thermal growth between steam piping, production piping, well heads, batteries headers, leading to severe steam leaks. Steam pipeline and piping are designed with anchors and guides to deal with thermal growth in the horizontal plane. When steam is charged at the ambient temperature, the cooling of the steam in long length pipelines and resulting condensate build up cause thermal gradient in the pipe wall. This thermal gradient coupled with transition in the piping and pipeline elevations are mainly responsible for the bowing, jumping and whipping phenomenon. Pressure, temperature and strain gauge instrumentation should be installed at strategic location to closely monitor and execute uniform warming up to avoid whipping, bowing, buckling and jumping of steam piping and pipelines. Every incident of whipping, bowing, buckling and jumping of steam piping & pipelines requires detailed integrity evaluation of the affected sections, prior to putting back into operation. Detailed assessment of wall thinning, ovality, dents and other mechanical damages are mandatory to comply with thin wall designs. The result in most incidents is complete replacement of the affected sections, requiring prolonged and costly shutdowns and risk to the producing reservoir due to lack of pressure.
机译:蒸汽管道和管道鞭打,鞠躬,屈曲和跳跃是本领域观察到的一些现象,由于设计不当和调试程序不足。结果,“蒸汽洪水”,“循环蒸汽刺激”和“SAGD”操作经历了长时间的蒸汽阻塞,延长的停机,生产损失和环境清洁蒸汽管道,直径为32英寸,长度为30公里,11 - 为80至100%的蒸汽质量的15MPa设计压力和250-340°设计温度,采用高强度材料和薄壁设计设计。虽然,设计是稳健的,但利用经过验证的压力分析工具,但经常无法解决在调试期间遇到的不平等变暖,冷凝水积聚和严重粘连的共同现场问题。而且,管路连接缺乏提供,以适应所需的热生长和/或蒸汽的管道之间的不相等的热生长,生产管道,井口,电池接头,导致严重蒸汽泄漏。蒸汽管道和管道采用锚和导轨设计,以处理水平面的热生长。当蒸汽在环境温度下充电时,长度管线的蒸汽冷却并导致冷凝物在管壁中产生热梯度。这种热梯度与管道和管道升降中的过渡相结合,主要负责弯曲,跳跃和鞭打现象。应在战略位置安装压力,温度和应变计仪表,以密切监测,并执行均匀的准备,以避免搅打,鞠躬,屈曲和跳跃蒸汽管道和管道。蒸汽管道和管道的每一次鞭打,弯曲,屈曲和跳跃都需要对受影响的部分进行详细的完整性评估,在重新开始运行之前。对墙壁变薄,椭圆形,凹痕和其他机械损坏的详细评估是强制性的,符合薄壁设计。大多数事件的结果是完全更换受影响的部分,由于缺乏压力,需要长时间和昂贵的停机和对生产的储层的风险。

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